CN202886162U - Combustion furnace for measuring total organic carbon - Google Patents
Combustion furnace for measuring total organic carbon Download PDFInfo
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- CN202886162U CN202886162U CN 201220544179 CN201220544179U CN202886162U CN 202886162 U CN202886162 U CN 202886162U CN 201220544179 CN201220544179 CN 201220544179 CN 201220544179 U CN201220544179 U CN 201220544179U CN 202886162 U CN202886162 U CN 202886162U
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- combustion furnace
- organic carbon
- total organic
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- determining total
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Abstract
The utility model relates to the field of measurement of total organic carbon and discloses a combustion furnace for measuring the total organic carbon. The combustion furnace comprises an interlayer outer shell, an insulating layer which is arranged in the interlayer outer shell, and a heating device, a furnace core through hole and a heat-conducting fan, which are arranged in the insulating layer. The interlayer outer shell is arranged in a closed combustion furnace chamber; an air outlet is arranged above the side wall of the combustion furnace chamber; the heat-conducting fan is arranged on the air outlet; an air inlet is formed in the bottom of the combustion furnace chamber; an air interlayer which is used for air flowing is arranged between the insulating layer and the interlayer outer shell; the furnace core through hole penetrates through the interlayer outer shell, the insulating layer and the heating device; a combustion tube is arranged in the furnace core through hole; an injection port and an exhaust port are formed in two ends of the combustion tube respectively; a carrier gas inlet is formed in the side wall of the injection port; and the injection port penetrates through the top wall of the combustion furnace chamber and is arranged outside of the combustion furnace chamber. The combustion furnace has the advantages of high oxidation rate, capability of continuous detection and separation of a high-temperature area in the combustion furnace from an external environment.
Description
Technical field
The utility model relates to the total organic carbon detection field, particularly a kind of combustion furnace for determining total organic carbon.
Background technology
Non-dispersive infrared absorption method is a kind of assay method comparatively commonly used of TOC water quality analytic apparatus of the total organic carbon (TOC) for dividing bleed.Use the method, only need once change, testing process is comparatively simple, and sensitivity is higher.Be worth different principle according to measuring TOC, non-dispersive infrared absorption method has can be divided into minusing and direct method.But no matter be minusing or direct method, all need first water sample to be measured is burnt with the carbon in the abundant oxidation water sample to be measured.In combustion process, combustion furnace is the core of TOC water quality analytic apparatus.In general, water sample to be measured need to react being higher than under 600 ℃ the temperature.The process that higher temperature of combustion can be accelerated to burn, accelerated reaction is carried out.
In the prior art, temperature can reach 900-1000 ℃ in the combustion furnace, although the heat-insulation layer insulation is arranged, it is outside that but furnace high-temperature still can arrive combustion furnace by conduction, affect the equipment of combustion furnace periphery, affected the accuracy of detection of combustion furnace pick-up unit, and too high also can have accelerated these and be attached to part on the combustion furnace and the aging speed of device.In addition, the combustion furnace internal temperature can only distribute by conduction, and the speed of distributing is excessively slow, and is difficult to carry out accurate temperature control, has affected burning rate and the stability of testing sample, can produce larger impact to last burning result.
In addition, the carbon content in can the Accurate Determining testing sample requires as far as possible fully oxidation testing sample of combustion furnace.Existing combustion furnace oxidation efficiency is not high, and some existing combustion furnace adopts the mode of cyclic oxidation for this reason, with the raising oxygenation efficiency, but has increased flow process yet, has strengthened inevitably error at measurment.
Summary of the invention
The utility model is too high for existing combustion furnace external temperature, accurate control combustion furnace interior temperature, the incomplete shortcoming of oxidation, providing a kind of can isolate combustion furnace internal high temperature district and external environment condition, can accurately control the combustion furnace internal temperature, have the novel combustion furnace of higher oxygenation efficiency.
For achieving the above object, the utility model can be taked following technical proposals:
The determining total organic carbon combustion furnace comprises the interlayer shell, is positioned at the heat-insulation layer of interlayer enclosure, the heating arrangement that is positioned at heat-insulation layer inside, combustion chamber through hole, heat conduction fan; Described interlayer shell is positioned at the combustion furnace chamber interior of sealing, burning furnace chamber sidewall top is provided with air outlet, be provided with the heat conduction fan on the air outlet, burning furnace chamber bottom is provided with air intake vent, is formed for the air buffer of Air Flow between described heat-insulation layer and the interlayer shell; Described combustion chamber through hole connects interlayer shell, heat-insulation layer, heating arrangement, be provided with flame tube in the described combustion chamber through hole, the two ends of flame tube are respectively arranged with injection port and exhausr port, and the sidewall of injection port is provided with carrier gas inlet, and injection port connects burning furnace chamber roof and be positioned at combustion furnace outdoor.
As preferably, the interlayer shell is respectively arranged with air vent in two ends up and down.
As preferably, flame tube is quartz glass tube.
As preferably, has the space between flame tube and the combustion chamber through hole.
As preferably, the combustion chamber through hole is cylindrical.
As preferably, the minimum clearance 〉=1cm of described air buffer.
As preferably, also comprise temperature sensor, the point for measuring temperature of temperature sensor is positioned at the inwall of the inner combustion chamber through hole of heating arrangement.
As preferably, described heat-insulation layer is high-temperature-resistant layer.
As preferably, be provided with temperature switch on the described interlayer shell.
As preferably, be provided with supporting layer in the flame tube, be filled with catalyzer between the supporting layer.
The utility model has significant technique effect owing to adopted above technical scheme:
The multiple tracks isolation barrier is set, prevents that the combustion furnace internal high temperature from affecting the combustion furnace working environment.Increased air buffer, make the air of air buffer inside circulate by the heat conduction fan that is arranged on the interlayer shell, take away the heat that combustion furnace distributes, realize the effect of isolation combustion furnace high-temperature region and extraneous low temperature environment, prevent that combustion furnace from producing harm to operating personnel.
The integral combustion stove is placed in the combustion furnace chamber interior of a sealing, and is further that high-temperature area and the combustion furnace working environment of combustion furnace inside is isolated.The injection port of flame tube connects burning furnace chamber roof, and it is outdoor to be positioned at the burning furnace chamber, and the convenient operation personnel add sample.
By being arranged on the heat conduction fan at the furnace chamber sidewall air outlet place of burning, can accelerate to burn furnace chamber and the interior circulation of air speed of air buffer, the air of forced burning furnace chamber and air buffer circulates to reduce the temperature of combustion furnace interlayer shell.
There is the space between combustion chamber through hole and the flame tube, is convenient to flame tube is inserted the combustion chamber through hole.
Be provided with the point for measuring temperature of temperature sensor on the combustion chamber through hole of combustion furnace, can carry out Accurate Measurement to the internal temperature of combustion furnace.Be arranged on temperature switch on the interlayer shell can be in the stove of combustion furnace temperature when surpassing design temperature, in time take urgent measure, cut off the power supply of heating arrangement.
In order to improve combustion efficiency, in flame tube, also be provided with catalyzer, between the two-layer supporting layer, this supporting layer can carry, support particles shape catalyzer about catalyzer was arranged on.Because sample to be tested is aqueous solution, therefore this supporting layer can play the effect of bearing sample to be tested, after sample to be tested injects flame tube by injection port, can be subject to the obstruct of supporting layer and catalyzer, and rapid steam raising, increased the residence time of sample to be tested in flame tube inside, improved contacting of catalyzer and sample to be tested, improved catalytic effect, the oxygenation efficiency in the testing sample can reach 99.5%.
Description of drawings
To be determining total organic carbon of the present utility model look synoptic diagram with the master of combustion furnace to Fig. 1.
Fig. 2 be Fig. 1 A-A to cross-sectional schematic.
Embodiment
Below in conjunction with embodiment the utility model is described in further detail.
The determining total organic carbon combustion furnace as shown in Figure 1, 2, comprises interlayer shell 1, is positioned at the heat-insulation layer 2 of interlayer shell 1 inside, the heating arrangement 3 that is positioned at heat-insulation layer 2 inside, combustion chamber through hole 4, heat conduction fan 5; Described interlayer shell 1 is positioned at burning furnace chamber 9 inside of sealing, and burning furnace chamber 9 sidewalls top is provided with air outlet, is provided with heat conduction fan 5 on the air outlet, and burning furnace chamber 9 bottoms are provided with air intake vent.
The interlayer shell is respectively arranged with air vent 11 in two ends about in the of 1.Be formed for the air buffer 6 of Air Flow between heat-insulation layer 2 and the interlayer shell 1, in order to guarantee the isolated effect of this air buffer 6, the minimum clearance of this air buffer 6 should 〉=1cm, the material of heat-insulation layer 2 is exotic material, and this exotic material should tolerate the high temperature more than 900 ℃ at least.
Described combustion chamber through hole 4 connects interlayer shell 1, heat-insulation layer 2, heating arrangement 3, is provided with flame tube 7 in the described combustion chamber through hole 4, and the material of flame tube 7 is quartz glass, and other similar high temperature resistant materials also can.Flame tube 7 is cylindrical with combustion chamber through hole 4, has certain space between flame tube 7 and the combustion chamber through hole 4.The two ends of flame tube 7 are respectively arranged with injection port 71 and exhausr port 72, and wherein injection port 71 is positioned at the upper end of flame tube 7, and exhausr port 72 is positioned at the bottom of flame tube 7.Injection port 71 is flat, be used for to the flame tube 7 inner samples to be tested that inject, it generally is aqueous solution, the injection port 71 of flat has larger cross-sectional area, can carry more sample to be tested, be convenient to the injection of sample to be tested, when the amount of sample to be tested is more, also can slow down the flow velocity that sample to be tested enters flame tube 7, improve the oxidation efficiency of flame tube 7.The sidewall of injection port 71 is provided with carrier gas inlet 74, is used for passing into the carrier gas such as oxygen.Injection port 71 connects burning furnace chamber 9 roofs and is positioned at outside the burning furnace chamber 9, and the convenient operation personnel add sample to be tested.
For the temperature of can Accurate Determining described determining total organic carbon with combustion furnace, prevent the combustion chamber excess Temperature, also be provided with temperature sensor 8 on the furnace wall, the point for measuring temperature of temperature sensor 8 is positioned at the inwall of heating arrangement 3 inner combustion chamber through holes 4.
Be provided with temperature switch 12 on the described interlayer shell 1.Temperature switch 12 is used for controlling the internal temperature that described determining total organic carbon is used combustion furnace.When described determining total organic carbon is higher than setting value with the internal temperature of combustion furnace, then temperature switch 12 cuts off described determining total organic carbon automatically with the power supplys of combustion furnace.
Be provided with supporting layer 73 in the flame tube 7, be filled with catalyzer between the two-layer supporting layer 73 up and down.
Through measuring, determining total organic carbon described in the utility model has higher oxidation efficiency with combustion furnace, the carbon in can the complete oxidation testing sample, and oxygenation efficiency can reach more than 99.5%.
In a word, the above only is preferred embodiment of the present utility model, and all equalizations of doing according to the utility model claim change and modify, and all should belong to the covering scope of the utility model patent.
Claims (10)
1. a determining total organic carbon combustion furnace is characterized in that, comprises interlayer shell (1), is positioned at the inner heat-insulation layer (2) of interlayer shell (1), is positioned at heat-insulation layer (2) inner heating arrangement (3), combustion chamber through hole (4), heat conduction fan (5); Described interlayer shell (1) is positioned at burning furnace chamber (9) inside of sealing, burning furnace chamber (9) sidewall top is provided with air outlet, be provided with heat conduction fan (5) on the air outlet, burning furnace chamber (9) bottom is provided with air intake vent, is formed for the air buffer (6) of Air Flow between described heat-insulation layer (2) and the interlayer shell (1); Described combustion chamber through hole (4) connects interlayer shell (1), heat-insulation layer (2), heating arrangement (3), be provided with flame tube (7) in the described combustion chamber through hole (4), the two ends of flame tube (7) are respectively arranged with injection port (71) and exhausr port (72), the sidewall of injection port (71) is provided with carrier gas inlet (74), and injection port (71) connects burning furnace chamber (9) roof and is positioned at outside the burning furnace chamber (9).
2. determining total organic carbon combustion furnace according to claim 1 is characterized in that, interlayer shell (1) up and down two ends is respectively arranged with air vent (11).
3. determining total organic carbon combustion furnace according to claim 1 is characterized in that, flame tube (7) is quartz glass tube.
4. determining total organic carbon combustion furnace according to claim 1 is characterized in that, has the space between flame tube (7) and the combustion chamber through hole (4).
5. determining total organic carbon combustion furnace according to claim 4 is characterized in that, combustion chamber through hole (4) is cylindrical.
6. determining total organic carbon combustion furnace according to claim 1 is characterized in that, the minimum clearance 〉=1cm of described air buffer (6).
7. determining total organic carbon combustion furnace according to claim 1 is characterized in that, also comprises temperature sensor (8), and the point for measuring temperature of temperature sensor (8) is positioned at the inwall of the inner combustion chamber through hole of heating arrangement (3) (4).
8. determining total organic carbon combustion furnace according to claim 1 is characterized in that, described heat-insulation layer (2) is high-temperature-resistant layer.
9. determining total organic carbon combustion furnace according to claim 1 is characterized in that, is provided with temperature switch (12) on the described interlayer shell (1).
10. determining total organic carbon combustion furnace according to claim 1 is characterized in that, is provided with supporting layer (73) in the flame tube (7), and supporting layer is filled with catalyzer between (73).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220544179 CN202886162U (en) | 2012-10-23 | 2012-10-23 | Combustion furnace for measuring total organic carbon |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220544179 CN202886162U (en) | 2012-10-23 | 2012-10-23 | Combustion furnace for measuring total organic carbon |
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| CN202886162U true CN202886162U (en) | 2013-04-17 |
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| CN 201220544179 Expired - Fee Related CN202886162U (en) | 2012-10-23 | 2012-10-23 | Combustion furnace for measuring total organic carbon |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102944454A (en) * | 2012-10-23 | 2013-02-27 | 杭州泰林生物技术设备有限公司 | Combustion furnace for total organic carbon determination |
-
2012
- 2012-10-23 CN CN 201220544179 patent/CN202886162U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102944454A (en) * | 2012-10-23 | 2013-02-27 | 杭州泰林生物技术设备有限公司 | Combustion furnace for total organic carbon determination |
| CN102944454B (en) * | 2012-10-23 | 2016-02-10 | 浙江泰林生物技术股份有限公司 | Combustion furnace for total organic carbon determination |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: ZHEJIANG TAILIN BIOTECHNOLOGY CO., LTD. Free format text: FORMER NAME: HANGZHOU TAILIN BIOTECHNOLOGY EQUIPMENT CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: 310052 Binjiang District, Zhejiang, South Ring Road, No. 2930, No. Patentee after: ZHEJIANG TAILIN BIOENGINEERING CO., LTD. Address before: 310052, No. 2930, South Ring Road, Hangzhou, Zhejiang, Hangzhou, Binjiang District Patentee before: Hangzhou Tailin Biotechnology Equipment Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130417 Termination date: 20191023 |